US4418204A - Method for making esters - Google Patents
Method for making esters Download PDFInfo
- Publication number
- US4418204A US4418204A US06/422,253 US42225382A US4418204A US 4418204 A US4418204 A US 4418204A US 42225382 A US42225382 A US 42225382A US 4418204 A US4418204 A US 4418204A
- Authority
- US
- United States
- Prior art keywords
- esters
- ester
- acid
- vacuum
- epoxy
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/12—Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
- C07D303/16—Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by esterified hydroxyl radicals
Definitions
- One process for the preparation of glycidyl esters is based on a reaction of the sodium or potassium salt of acrylic or methacrylic acid with epichlorohydrin (U.S. Pat. Nos. 2,556,075 and 2,537,981), optionally with the addition of catalytic amounts of tetramethylammonium chloride.
- the charge may further contain auxiliary agents such as stabilizers, for example, hydroquinone monomethyl ether, hydroquinone, phenothiazine, or N,N'-diphenyl-para-phenylenediamine.
- auxiliary agents such as stabilizers, for example, hydroquinone monomethyl ether, hydroquinone, phenothiazine, or N,N'-diphenyl-para-phenylenediamine.
- the process may be carried out in the following manner, for example:
- the alcohol distillate (methyl methacrylate in azeotropic mixture with methanol) starts to pass over at an overhead temperature of about 30° to 36° C. As soon as no further alcohol distillate is observed, excess methyl methacrylate is drawn off at an increased overhead temperature (about 50° C.).
- the residual crude ester can be substantially degassed, that is to say, freed of methyl methacrylate. The degassed crude ester can then be vacuum distilled. A pure product is obtained in a very good yield.
- a mixture of 70.0 kg (945 moles) of glycidol, 280 kg (2800 moles) of methyl methacrylate, 120 ppm of 1,4-diazabicyclo(2,2,2)octane, 30 ppm of KOH (in methanol), and 200 ppm of N,N'-diphenyl-para-phenylenediamine (as a stabilizer) is charged into a 500-liter V4A agitated vessel having a 4-meter steel column packed with porcelain Raschig rings and equipped with water and brine reflux condenser, interchangeable receiver, reflux control, and vacuum control. A vacuum is produced and the vessel is heated by means of circulating hot water. At a vessel temperature of 60° C.
- a distillate starts passing over from the alcoholysis with a reflux ratio of 2:1.
- the vessel temperature rises to 70° C., and the overhead temperature is held between 33° and 36° C. by adjustment of the reflux ratio of 5:1.
- unreacted methyl methacrylate is withdrawn at a reflux ratio of 1:1 and a temperature of 50° C.
- the crude glycidyl methacrylate ester formed can be degassed down to a residual gas content of about 10%. After further degassing at 110° C.
- the ester formed in the vapor space and a vacuum of 30 mm Hg, can be distilled at 115° C. in the vapor space and 1 to 2 mm Hg. Yields over 80% are observed.
- the total time usually ranges from about 6 to 9 hours.
- a mixture of 475 g (6,41 moles) of glycidol, 2000 g (20 Mol) of methyl methacrylate 200 ppm of 1,4-diazabicyclo(2,2,2)octane and 200 ppm of N,N'-diphenyl-p-phenylenediamine (as a stabilizer) is charged into a 4-liter agitated glass vessel having a 1 meter glass column packed with glass Raschig rings and equipped with a water and a brine reflux condenser, interchangeable receiver, reflux control and vacuum control. A vacuum is produced and the vessel is heated by means of circulating hot water. At a vessel temperature of 60° C.
- a distillate starts passing over from the alcoholysis with a reflux ratio of 2:1.
- the vessel temperature rises to 70° C., and the overhead temperature is held between 33° and 36° C. by adjustment of the reflux ratio of 5:1.
- unreacted methyl methacrylate is withdrawn at a reflux ratio of 1:1 and a temperature of 50° C.
- the crude glycidyl methacrylate ester formed can be degassed down to a residual gas content of about 10%. After further degassing at 110° C.
- the ester formed in the vapor space and a vacuum of 30 mm Hg, can be distilled at 115° C. in the vapor space and 1 and 2 mm Hg. Yields over 80% are observed.
- the total time usually ranges from about 6 to 9 hours.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Epoxy Compounds (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3140764 | 1981-10-14 | ||
DE19813140764 DE3140764A1 (de) | 1981-10-14 | 1981-10-14 | Verfahren zur herstellung der ester vopn carbonsaeuren mit epoxigruppenhaltigen alkoholen |
Publications (1)
Publication Number | Publication Date |
---|---|
US4418204A true US4418204A (en) | 1983-11-29 |
Family
ID=6144064
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US06/422,253 Expired - Lifetime US4418204A (en) | 1981-10-14 | 1982-09-23 | Method for making esters |
Country Status (6)
Country | Link |
---|---|
US (1) | US4418204A (enrdf_load_stackoverflow) |
JP (1) | JPS5872576A (enrdf_load_stackoverflow) |
DE (1) | DE3140764A1 (enrdf_load_stackoverflow) |
FR (1) | FR2514356B1 (enrdf_load_stackoverflow) |
GB (1) | GB2107319B (enrdf_load_stackoverflow) |
IT (1) | IT1156520B (enrdf_load_stackoverflow) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5527927A (en) * | 1994-05-20 | 1996-06-18 | Mitsubishi Gas Chemical Company, Inc. | Process for producing glycidyl acrylate or glycidyl methacrylate |
CN103214435A (zh) * | 2013-03-20 | 2013-07-24 | 沈阳金久奇科技有限公司 | 一种制备甲基丙烯酸缩水甘油酯的方法 |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2537981A (en) * | 1949-10-28 | 1951-01-16 | American Cyanamid Co | Method of producing a glycidyl ester |
US2556075A (en) * | 1948-06-19 | 1951-06-05 | American Cyanamid Co | Method of polymerizing glycidyl compounds |
GB1118206A (en) | 1964-12-22 | 1968-06-26 | British Petroleum Co | Preparation of epoxy esters |
FR2088971A5 (en) | 1970-04-30 | 1972-01-07 | Ugilor | Methacrylic and acrylic esters - from higher alcohols by transesterification using thallium alcoholate catalyst |
DE2602157A1 (de) | 1975-01-24 | 1976-07-29 | Ciba Geigy Ag | Verfahren zur herstellung von polycarbonsaeurepolyglycidylestern |
US4074062A (en) * | 1975-08-21 | 1978-02-14 | Mitsubishi Rayon Company, Limited | Process for producing unsaturated carboxylic acid esters |
US4228084A (en) * | 1975-06-05 | 1980-10-14 | Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler | Process for the production of glycidyl methacrylate |
US4285872A (en) * | 1977-06-06 | 1981-08-25 | Nippon Oil And Fats Company, Ltd. | Method for producing glycidyl (metha)acrylate |
DE2423405C3 (de) | 1974-05-14 | 1983-05-19 | Degussa Ag, 6000 Frankfurt | Verfahren zur Herstellung von Glycidylmethacrylat |
-
1981
- 1981-10-14 DE DE19813140764 patent/DE3140764A1/de active Granted
-
1982
- 1982-09-07 FR FR8215158A patent/FR2514356B1/fr not_active Expired
- 1982-09-10 IT IT8268081A patent/IT1156520B/it active
- 1982-09-23 US US06/422,253 patent/US4418204A/en not_active Expired - Lifetime
- 1982-10-08 JP JP57176441A patent/JPS5872576A/ja active Granted
- 1982-10-13 GB GB08229292A patent/GB2107319B/en not_active Expired
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2556075A (en) * | 1948-06-19 | 1951-06-05 | American Cyanamid Co | Method of polymerizing glycidyl compounds |
US2537981A (en) * | 1949-10-28 | 1951-01-16 | American Cyanamid Co | Method of producing a glycidyl ester |
GB1118206A (en) | 1964-12-22 | 1968-06-26 | British Petroleum Co | Preparation of epoxy esters |
FR2088971A5 (en) | 1970-04-30 | 1972-01-07 | Ugilor | Methacrylic and acrylic esters - from higher alcohols by transesterification using thallium alcoholate catalyst |
DE2423405C3 (de) | 1974-05-14 | 1983-05-19 | Degussa Ag, 6000 Frankfurt | Verfahren zur Herstellung von Glycidylmethacrylat |
DE2602157A1 (de) | 1975-01-24 | 1976-07-29 | Ciba Geigy Ag | Verfahren zur herstellung von polycarbonsaeurepolyglycidylestern |
US4228084A (en) * | 1975-06-05 | 1980-10-14 | Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler | Process for the production of glycidyl methacrylate |
US4074062A (en) * | 1975-08-21 | 1978-02-14 | Mitsubishi Rayon Company, Limited | Process for producing unsaturated carboxylic acid esters |
US4285872A (en) * | 1977-06-06 | 1981-08-25 | Nippon Oil And Fats Company, Ltd. | Method for producing glycidyl (metha)acrylate |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5527927A (en) * | 1994-05-20 | 1996-06-18 | Mitsubishi Gas Chemical Company, Inc. | Process for producing glycidyl acrylate or glycidyl methacrylate |
CN103214435A (zh) * | 2013-03-20 | 2013-07-24 | 沈阳金久奇科技有限公司 | 一种制备甲基丙烯酸缩水甘油酯的方法 |
Also Published As
Publication number | Publication date |
---|---|
DE3140764A1 (de) | 1983-04-28 |
GB2107319B (en) | 1985-09-11 |
FR2514356A1 (fr) | 1983-04-15 |
DE3140764C2 (enrdf_load_stackoverflow) | 1990-03-01 |
JPS5872576A (ja) | 1983-04-30 |
GB2107319A (en) | 1983-04-27 |
JPH0321027B2 (enrdf_load_stackoverflow) | 1991-03-20 |
FR2514356B1 (fr) | 1987-04-24 |
IT8268081A0 (it) | 1982-09-10 |
IT1156520B (it) | 1987-02-04 |
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